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One of the developments of the situation is that the Tariff Commission is very much opposed to administering any licensing system. It came to the ears of the Commission that it had been suggested as the proper body to administer the licensing machinery, and the

ing mining engineer for the American International Corporation. The present headquarters of the International Exposition of Mining Industries is Room 421, 405 Lexington Ave., New York.

result was that the Commission not only reiterated its Peace Treaty Provisions Regarding German

opposition to most of the licensing suggestions, but emphatically urged that it not be selected to administer any of the licenses.

Dr. Hoyt S. Gale of the Geological Survey, in testifying this week before the House Ways and Means Committee, said that the German potash industry could not regain the position it held before the war. The increased cost of labor and the internal condition of the industry, he said, were such that German potash would have to sell for at least $1.50 per unit.

Dr. Gale returned to Washington last week from Europe, where he made a study of the potash industry, and it was at the special request of Secretary Lane that the Ways and Means Committee summoned him to testify.

W. E. Sharp, president of the Western Potash Works and of the American Potash Co. of Lincoln, Neb., denied to the Committee that the potash industry of this country was controlled by the packers. He admitted, however, that one company was owned by the packers, but said that the products of that company were used by the owners in the manufacture of fertilizer.

The hearings on potash and dyestuffs before the House Ways and Means Committee will not be resumed until after the House recess, Sept. 8.

International Exposition of Mining
Industries

A permanent exhibit of mining and metallurgical machinery is to be established under the direction of the Merchants and Manufacturers Exchange of New York, which has taken over Grand Central Palace for the purpose of maintaining industrial exhibits of various kinds. Approximately 50,000 sq.ft. of space, or one entire floor, will be devoted to the machinery and supplies used in the development and operation of metal mines, non-metal mines, coal mines and oil wells; subsequent extraction or refining of the raw products by concentration, leaching, cyaniding, flotation, smelting, distillation, coking, etc.

The new enterprise enjoys unusual support in the backing of the Nemours Trading Corporation, of which Alfred I. duPont is president. The corporation owns and controls the Merchants and Manufacturers Exchange of New York and has branches in the leading cities of the world consisting of 19 branch offices and 3000 foreign selling agents. The purpose and function of the venture are to develop both foreign and domestic trade in all lines of industry and to establish at a central point a permanent exhibit of machinery and products for the benefit of foreign and domestic merchants.

The exhibit of mining industries will include aërial and surface transportation, laboratory appliances and supplies, blast-furnaces and other ore-treating equipment, compressors, crushers, concentrating machinery, hoists, drills, power machinery, ventilating equipment, etc. The exhibition will be under the direct management of Mr. Howard R. Ward, a mining engineer who prior to entering war work was for three years consult

Dyes and Chemicals

The War Trade Board Section of the Department of State quotes, for the information of those concerned, the following provisions of the Treaty of Peace relative to German dyes and chemicals:

ANNEX VI

1. Germany accords to the Reparation Commission an option to require as part of reparation the delivery by Germany of such quantities and kinds of dyestuffs and chemical drugs as the Commission may designate, not exceeding 50 per cent of the total stock of each and every kind of dyestuff and chemical drug in Germany or under German control at the date of the coming into force of the Treaty.

This option shall be exercised within sixty days of the receipt by the Commission of such particulars as to stocks as may be considered necessary by the Commission.

2. Germany further accords to the Reparation Commission an option to require delivery during the period from the date of the coming into force of the present Treaty until Jan. 1, 1920, and during each period of six months thereafter until Jan. 1, 1925, of any specified kind of dyestuff and chemical drug up to an amount not exceeding 25 per cent of the German production of such dyestuffs and chemical drugs during the previous six months period. If, in any case the production during such previous six months was, in the opinion of the Commission, less than normal, the amount required may be 25 per cent of the normal production.

Such option shall be exercised within four weeks after the receipt of such particulars as to production and in such form as may be considered necessary by the Commission; these particulars shall be furnished by the German Government immediately after the expiration of each six months period.

3. For dyestuffs and chemical drugs delivered under paragraph 1, the price shall be fixed by the Commission, having regard to pre-war net export prices and to subsequent increases of cost.

For dyestuffs and chemical drugs delivered under paragraph 2, the price shall be fixed by the Commission, having regard to pre-war net export prices and subsequent variations of cost, or the lowest net selling price of similar dyestuffs and chemical drugs to any other purchaser.

4. All details, including mode and times of exercising the options, and making delivery, and all other questions arising under this agreement shall be determined by the Reparation Commission; the German Government will furnish to the Commission all necessary information and other assistance which it may require.

5. The above expression "dyestuffs and chemical drugs" includes all synthetic dyes and drugs and intermediate or other products used in connection with dyeing, so far as they are manufactured for sale. The present arrangement shall also apply to cinchona bark and salts of quinine.

German-Owned Chemical Plants Sold

The largest single day's sale of German-owned property was made at public auction on July 18 by the Alien Property Custodian. The sale of three chemical plants brought $4,419,980. The successful bidders were W. E. Coffin & Co. and the American Analine Products, Inc., of 80 Fifth Ave., New York.

The Roessler & Hasslacher Chemical Co., of 100 William Street, New York City, with plants at Perth Amboy, N. J., and St. Albans, W. Va., was bought in at $505 a share. The stock of the Niagara Electro Chemical Co. sold at $4000 a share, the total price being $440,000. The concern has offices at 100 William Street, New York, and plants at Perth Amboy, N. J., and Niagara Falls, N. Y. The Perth Amboy Chemical Co. stock went for $940,800, or $480 a share.

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FIG. 1.

GENERAL VIEW OF PLANT OF MINNESOTA BY-PRODUCT COKE CO., ST. PAUL, MINN. From the left are: Coal crushing tower, stack, housing for inclined coal conveyor from coal dumping building in center foreground to top of the coal crushing tower, housing for inclined coal conveyor from bottom of coal crushing tower to top of coal storage bins at end of Battery B, from which bins the larry car is loaded with coal to be charged into the ovens. In the lefthand background are the two batteries totaling 65 ovens. To right of battery storage bins in order are: By-product buildings, rich and lean gas holders, final gas coolers and light oil scrubbers.

The Coking of Illinois Coal in Koppers Type Oven*

An Operating Test at the St. Paul Plant of Minnesota By-Product Coke Company Conducted Jointly by the National Bureau of Standards and the United States Bureau of Mines for Coking Orient, Franklin County, Ill., Coal

T

BY R. S. MCBRIDE+ AND W. A. SELVIG

HE great importance during the war period of substituting Mid-Continent coal for coals from more distant sources even in by-product coke-oven work was well recognized. The Bureau of Standards was ordered to conduct an investigation of a new cokeoven process claimed to be especially suited to this purpose, and in connection with this the Bureau was requested to conduct a test of the St. Paul plant of the Minnesota By-Product Coke Co., which is owned by the Koppers Co., Pittsburgh. The Bureau of Standards, in co-operation with the Bureau of Mines, carried out this operating test, using during 7 days about 7700 tons of coal from the Orient Mine, Franklin County, Illinois.

The plant is usually operated with a mixture of Pittsburgh, Elkhorn and Pocahontas coal at normal coking times of about 16 and 17 hr. The normal capacity of the plant is approximately 1100 tons of coal per day. For the test period only Orient coal was used. Since the coking time for this coal was slightly longer than for the usual mixture, the capacity of the plant was reduced somewhat.

All phases of coal handling, by-product recovery and laboratory tests were under observation by the staff of

This is an advance publication in abbreviated form of Bureau of Standards Technologic Paper No. 137. Published by permission of the Directors, Bureau of Standards and Bureau of Mines. + Engineer chemist, Bureau of Standards. Assistant chemist, Bureau of Mines.

37 Government engineers and chemists employed on the work. In addition, those in charge had the benefit of advice and comment from a considerable number of experts who are specialists in the field of coke-oven operation. The quantity of all coal used and of all byproducts obtained was carefully weighed or measured at regular intervals and samples of each material were taken for analysis. The Bureau of Standards was responsible for the general planning and supervision of the test work. Its representatives made all observations of battery operation, high temperature measurements, by-product recovery, and chemical laboratory work on gas and by-products. The Bureau of Mines was responsible for the sampling of the coal both as it was loaded at the mine and as crushed at the plant. It supervised the weighing, coal-handling, coke-handling and coke-sampling operations and made all analyses of coal and coke. Its representatives also made general observations on the character of the coke and operation of the ovens.

The Minnesota By-Product Coke Company plant consisted of 65 ovens, built with a gross regenerative system, operating during the test period with an average gross coking time of 19 hr. and 33 min., with coal finely pulverized, 12.75 tons per oven as charged. Each oven was 39 ft. long, 9 ft. high, 17 in. wide at the pusher side and 19 in. at the coke side, making a 21-in. taper with an average width of 18 in. The coke was

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In the foreground from left to right are shown: Coke wharf, housings for the coke conveyors, the first screening station where large furnace coke is separated from run of oven coke, and the housing for the inclined coke conveyor to final screening station, where the coke is further separated into small furnace and domestic sizes. In the background are the final gas coolers and light oil scrubbers, shown also in Fig. 1, the power plant, laboratory, complete light oil refining buildings, and coke-quenching station.

discharged from the ovens by the usual style of ram pusher into the common form of hot coke car and quenched in a tower of the usual kind. After discharge on the wharf it was handled by a typical conveyor system through two screening stations. The coke was screened to produce large and small furnace sizes; stove, nut and pea, domestic sizes and breeze. The gas was separated into rich and lean at the battery. Separate test records were kept of each size of coke and of each quality of gas. Practically all of the ammonia produced was made up into sulphate immediately through the direct recovery process. Although the plant operated for the production of pure light-oil products, only the total production of light oil was measured, but the yield of various constituents was determined by analysis.

COAL USED

The coal was apparently clean and very well screened. The impurities consisted of a small amount of pyrite, mostly in the form of thin layers, calcite, mother of coal, and shale. The coal was crushed at the plant with the intention of making it as fine as was feasible with the apparatus available. As charged to the ovens, over 95 per cent passed through a 4-mesh sieve, and about two-thirds passed through a 10-mesh sieve.

A composite sample of the crushed coal sampled from the conveyor belt was made up from the daily plant samples and analyzed according to the laboratory methods described in Bureau of Mines Technical Paper No. 8; the results are presented in Table I.

In Table II is given the total amount of coal used and the average coking time for the period of the test.

PUSHING AMPERAGE

No consecutive record was maintained of the current necessary to push the oven charges. However, sufficient data were obtained to show that, in general, the charges pushed easily, though not as easily as with the usual coal mixture. It generally required from 180 to 250 amp. to start the charge and from 120 to 180 amp.

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mass and in the vapor above the coal. Measurement of high temperatures in a by-product coke oven is attended with great difficulty because of the inaccessibility of certain points where temperature measurements are desirable and because of the limited variety and high cost of apparatus which can be used for these purposes. The results obtained are sufficient, however, to give an accurate idea of the range and average temperature maintained at the important points in the heating system.

A complete survey of temperature conditions through the entire battery was, of course, impossible; but rep

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resentative points were chosen and the results given in Figs. 3 to 6 inclusive are typical of all operations. During the period of the test certain optical pyrometer measurements were made by the company engineers which confirmed the fact that the locations chosen for our regular measurements were typical.

The general trend of heating wall temperatures, before, during and after charging the adjoining ovens, is given in Fig. 3. These temperatures, of course, are not as high as prevail in certain parts of the wall refractory, for example at the lower regulating brick near the air port, where the maximum temperature is reached. To show the effect of gas and air reversal on the temperature in the heating wall, the curve of Fig. 4 is given.

Temperature measurements were made at three places in four consecutive charges of coal in oven No. 3. Readings were taken with couples 10 ft. long, introduced through charging lids as nearly as possible midway between the oven walls. The mean of the temperature-time curves for these locations is plotted in Fig. 5. Short thermocouples were introduced through the charging lid nearest the pushing end of oven No. 3 to measure the vapor above the coal. Four curves for four consecutive charges are shown in Fig. 6.

Over the checker-brick in the right half of the regenerator under oven No. 3 at the coke and 54 in. in from the face of the regenerator wall the temperature averaged 1140 deg. C. The variation in temperature during reversal of direction of gas burning was about 55 deg. C. at this point. Temperature measurements taken at the junction of the waste heat tunnels from the two batteries averaged 272 deg. C.

COKE HANDLING

During the test, two different systems of screening were used as follows:

Screening System No. 1-The coke was delivered by the conveyor over an inclined-bar-grizzly screen in the first station. The screen was about 5 ft. long, 4 ft.

wide and consisted of 11-in. bars spaced from 14 to 11⁄2 in. The oversize was delivered in the railroad cars and weighed as "furnace coke." The undersize delivered on a second belt conveyor was carried to a second screening station, where it passed through an inclined-rotarycylindrical screen, the first half of which consisted of -in. square perforations, and the second half 13-in. square perforations. The material passing through the -in. perforations was re-screened on a 1-in. shaker screen to separate the breeze and pea size coke. The material passing through the 18-in. perforations was called nut coke, and that passing over the 18-in. perforations was classified as stove coke. The breeze, pea, nut and stove sizes were separately loaded in railroad cars and weighed before shipment or storage. Nut and stove sizes, as delivered from their respective bins, passed over shaker feeders before going into the railroad cars. The pea and breeze sizes were thus very completely eliminated from these two domestic sizes. Since the separation of "furnace coke" by the inclined-bar-grizzly in the first screening station was not considered satisfactory because the screen was not large enough to handle the quantity of coke passing over it and make a good separation, a change was made after three days of the test to the second system, which was as follows:

Screening System No. 2-The inclined-bar-grizzly in the first screening station was discarded and replaced by a 21-in. rotary grizzly, the oversize of which was delivered directly into railroad cars as "foundry" or "large furnace" coke. The coke passing through the first rotary grizzly was carried to the second screening station, where it passed over a second rotary grizzly set at 13 in. The oversize of this second grizzly was designated as "small furnace" coke. The material passing

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through the second grizzly was separated by the rotary cylindrical screen and sized exactly as in the first system. The furnace coke from the first system and both sizes of furnace coke from the second system, after being weighed, were stacked in a pile at the plant during the test period, so that they were subsequently available for a blast-furnace test as described later. The stove, nut and pea sizes were sold for domestic fuel, as is customary from this plant. The breeze produced was used as boiler fuel at the plant, following the regular practice.

COKE YIELDS

Table III shows the different results obtained from the two screening methods. The results for the entire period are summarized together in Table IV.

It is to be noted that 82.7 per cent of the dry coke produced in screening system No. 1 was classified as furnace coke, oversize of the 11- to 12-in. inclined-bar grizzly. As explained under description of screening system No. 1, the separation of the furnace coke by the inclined-bar grizzly was not considered satisfactory, as the screen was not large enough to make a good

TABLE III-RESULTS WITH TWO SCREENING SYSTEMS

Screening
System No. 2,
Per Cent

included in the furnace size if it had been possible to install a 1-in. inclined-grizzly-bar screen large enough to handle the coke produced and make a good separation. The small percentage of large-size coke obtained together with the large percentage of the smaller domestic sizes indicated that it would not stand handling and screening without breaking up into smaller pieces, due to the fingery and brittle characteristics of the coke. APPEARANCE OF HOT COKE

The hot coke as pushed from the ovens was observed in order to know the temperature and general performance of each oven and each lot was again observed after

Screening
System No. 1,
Per Cent

Furnace Sizes:

Large.

18.3

Small.

22.0

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Time - Hours after Charging TEMPERATURE OF VAPOR ABOVE COAL

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quenching and dumping on the wharf. By these observations a very complete idea of battery performance was obtained. These observations may be summarized as follows:

The top of the coke mass was, as usual, colder than the rest of the charge. In fact this condition was somewhat exaggerated during the test, as it was impracticable to adjust the battery for the best use of the leaner gas from the Illinois coal when this was to be used for so short a period. From the level of the horizontal flue in the heating wall down to the bottom of the oven the coal was usually thoroughly coked; and in general the heats were uniform for the entire length of the charge. From a number of the charges some uncoked material remained in the center of the charge at the level of the horizontal flue.

From most of the charges a large amount of smoke 1292 g and flame arose as the coke was pushed from the oven; this was especially noticeable in cases where uncoked material remained at the level of the horizontal flue. The overhang of the coke as it fell from the coke guide into the quenching car was irregular; on the coke side it ranged from 12 to 24 in., while on the pusher side the coke frequently showed signs of crumbling. Immediately ahead of the pusher ram the charge generally crumbled, thus causing a great deal of fine coke. A distinct line of cleavage was noted through the center of the charge in almost all cases.

1112

932

752

572

392

212

32

FIG. 5. AVERAGE OF COAL TEMPERATURE CURVES

separation; the very high percentage obtained for furnace size is, therefore, not representative. The total dry furnace coke was only 40.3 per cent of the total dry coke screened during that part of the test when screening system No. 2 was used. However, it should be noted that the yield of stove size is very large, 34.8 per cent of the total coke as screened; there is no doubt that a large amount of the stove size would have been

APPEARANCE OF COKE ON WHARF AND IN CARS The coke on the wharf was very irregular in size, but on the average the pieces were distinctly smaller than for the average by-product coke mixtures. There was no tendency to blockiness and very few pieces were as large as 6 in. in each dimension. The material was decidedly lighter than the average by-product oven coke, weighing only about 23 lb. per cu.ft. The color varied somewhat, but in general the furnace-size was of a dark silver color.

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